WO2013047177A1 - Powder and granular material separation processing device, powder and granular material separation processing method, and powder and granular material separation and recovery processing system - Google Patents

Powder and granular material separation processing device, powder and granular material separation processing method, and powder and granular material separation and recovery processing system Download PDF

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WO2013047177A1
WO2013047177A1 PCT/JP2012/073124 JP2012073124W WO2013047177A1 WO 2013047177 A1 WO2013047177 A1 WO 2013047177A1 JP 2012073124 W JP2012073124 W JP 2012073124W WO 2013047177 A1 WO2013047177 A1 WO 2013047177A1
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separation
granular material
suction
mixture
powder
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PCT/JP2012/073124
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French (fr)
Japanese (ja)
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智昭 徳田
山本 修司
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株式会社カシワバラ・コーポレーション
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Priority claimed from JP2011213978A external-priority patent/JP5583100B2/en
Priority claimed from JP2012001781U external-priority patent/JP3176156U/en
Application filed by 株式会社カシワバラ・コーポレーション filed Critical 株式会社カシワバラ・コーポレーション
Priority to US14/347,398 priority Critical patent/US9254508B2/en
Publication of WO2013047177A1 publication Critical patent/WO2013047177A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B4/00Separating solids from solids by subjecting their mixture to gas currents
    • B07B4/02Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall
    • B07B4/04Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall in cascades
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B4/00Separating solids from solids by subjecting their mixture to gas currents
    • B07B4/02Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B7/00Selective separation of solid materials carried by, or dispersed in, gas currents
    • B07B7/01Selective separation of solid materials carried by, or dispersed in, gas currents using gravity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B7/00Selective separation of solid materials carried by, or dispersed in, gas currents
    • B07B7/04Selective separation of solid materials carried by, or dispersed in, gas currents by impingement against baffle separators

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  • Combined Means For Separation Of Solids (AREA)

Abstract

[Purpose] To introduce a mixture to be processed, in which powder and granular material with comparatively large specific gravity and hardness and lightweight foreign substances that come along with the same have been mixed, into a system and separate the same by a dry method. [Solution] A powder and granular material separation processing device (X) wherein a dust collection device, electric vacuum cleaner, or other external suction machine is connected thereto, and a mixture to be processed is introduced by suction to a separation processing vessel (1) and, along with recovering the powder and granular material within the system, lightweight foreign substances are discharged outside of the system. The separation processing vessel (1) is provided with a suction introduction tube (2) that receives the mixture to be processed on the circumferential surface and is attached and sealed as an upper part structure of a hopper tank (4) that collects and stores the powder and granular material, and a suction discharge tube (3) that is connected to the external suction machine is provided on the upper surface of the vessel. In addition, the separation processing vessel (1) has a separation cone (11), the bottom surface of which is formed into a funnel shape, and a cylindrical opening (13) that hangs in a protruding shape downward from the tip part of the separation cone (11) and for which the opening diameter thereof is formed with a stepwise reduction. The tip part of the suction discharge tube (3) has a multiple pipe constitution, and each pipe is given a pipe diameter smaller than the opening diameter for the cylindrical opening (13), is loosely inserted, and approaches the tip part of the opening.

Description

粉粒体分離処理装置及び粉粒体分離処理方法並びに粉粒体分離回収処理システムPOWDER PARTICLE SEPARATING PROCESSING APPARATUS, POWDER PARTICLE SEPARATING TREATMENT METHOD, AND POWDER PARTICLE SEPARATING COLLECTION
 本発明は、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を系内導入し、乾式で前記粉粒体と前記軽量異物類とを分離処理する粉粒体分離処理装置及び粉粒体分離処理方法並びに粉粒体分離回収処理システムに関する。 The present invention is based on a mixture to be treated in which a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less, and light-weight foreign substances accompanied therewith are mixed. The present invention relates to a granular material separation processing apparatus, a granular material separation processing method, and a granular material separation and recovery processing system, which are introduced into the inside and dry-process the separation of the granular material and the lightweight foreign substances.
 より詳しくは、第1の基礎出願(特願2011-213978号)に係る本発明は、集塵装置や電気掃除機等の外部吸引機器に接続した分離処理容器内に前記被処理混合物を吸引導入し、該容器内で流動を制御しながら気流と比重差を利用して分離処理し、前記粉粒体を系内回収するとともに、前記軽量異物類を前記外部吸引機器に向けて系外排出するための粉粒体分離処理装置及び粉粒体分離処理方法に関する。 More specifically, the present invention according to the first basic application (Japanese Patent Application No. 2011-213978) introduces the mixture to be treated by suction into a separation container connected to an external suction device such as a dust collector or a vacuum cleaner. Then, separation is performed using an air flow and a specific gravity difference while controlling the flow in the container, the powder particles are collected in the system, and the lightweight foreign matters are discharged out of the system toward the external suction device. The present invention relates to a granular material separation processing apparatus and a granular material separation processing method.
 また、第2の基礎出願(実願2012-1781号)に係る本発明は、上記粉粒体分離処理装置を装置系の一構成装置として包含し、該粉粒体分離処理装置にバキューム接続する前・後流の連係機器(装置)をプラットフォームとなる単一の枠体内に収設し、かつ、工程順にライン配置して系統的な処理をおこなうようにした粉粒体分離回収処理システムに関する。なお、装置系とシステムの用語は互換的に使用する。 Further, the present invention according to the second basic application (Japanese Patent Application No. 2012-1781) includes the above-described powder / particle separation processing apparatus as one apparatus of the apparatus system, and is vacuum connected to the powder / particle separation processing apparatus. The present invention relates to a granular material separation / recovery processing system in which front / rear linked devices (devices) are housed in a single frame as a platform, and are arranged in a line in the order of processes to perform systematic processing. Note that the terms system and system are used interchangeably.
 本発明が扱う被処理混合物の代表的な例として、乾式エアーブラスト装置によるブラスト工程を経た研削材(粉粒体)と、これに同伴される軽量異物類からなるものを挙げることができる。この研削材(粉粒体)と軽量異物類の比重はともに1桁であり、かつ、両者の比重差は比較的小さいといえる。 As a typical example of the mixture to be treated which is handled by the present invention, there can be mentioned a material made of a grinding material (powder) subjected to a blasting process by a dry air blasting apparatus and light-weight foreign substances accompanied therewith. It can be said that the specific gravity of the abrasive (powder particles) and the light-weight foreign matter are both single digits, and the specific gravity difference between the two is relatively small.
 ここで、研削材は金属系と非金属系に大別される。金属系研削材は所謂スチールグリットやスチールショットと称される鋳鉄や鋳鋼の粉粒体である。非金属系研削材は天然鉱物や造鉱物のグリット状又はショット状の粉粒体である〔必要ならば、JISZ0310素地調整用ブラスト処理方法通則の研削材の項を参照〕。 Here, abrasives are roughly divided into metallic and non-metallic. The metal-based abrasive is a so-called steel grit or steel shot called cast iron or cast steel powder. The non-metallic abrasive is a grit-like or shot-like powder of a natural mineral or an artificial mineral (see the section of abrasive in the general blasting method for JIS Z0310 substrate adjustment if necessary).
 なお、グリット[grit]とは角張った形状の粒子、ショット[shot]とは角張りが少ない形状の粒子を指称するものである。 In addition, the grit [grit] refers to particles having an angular shape, and the shot [shot] refers to particles having a less angular shape.
 従来より、容器類や家電製品廃棄物、情報機器廃棄物などから発生する廃棄プラスチック類を再生樹脂として回収処理するために、粒子径を10mm以下に破砕処理し、且つ劣化表面層の剥離を主目的にして乾式洗浄処理した後の紙片等の軽量異物類を多数含有するブラスチック破砕粒状体を被処理混合物とするサイクロン型気流応用分離装置が知られている(例えば、特許文献1を参照)。 Conventionally, in order to recover waste plastics generated from containers, household electrical appliance waste, information equipment waste, etc. as recycled resin, the particle diameter is crushed to 10 mm or less, and peeling of the deteriorated surface layer has been mainly performed. 2. Description of the Related Art A cyclone type air flow application separation apparatus is known that uses a plastic crushed granule containing a large number of lightweight foreign matters such as paper pieces after dry cleaning for the purpose of treatment (see, for example, Patent Document 1). .
 なお、サイクロン型とは、粉塵含有気体(被処理混合物含有気体に同じ)を旋回させて該気体中から粉粒体等を遠心分離して捕集又は分級する分離方式をいう。 The cyclone type refers to a separation method in which a dust-containing gas (same as the gas to be treated-containing gas) is swirled to collect or classify particles and the like by centrifugation.
 ここでみるべき点は、円筒部内で遠心降下粒状体含有気流を、中央に開口部を有する仕切板によって気流排出管の先端開口の下部空間部へ急激に流速を高めた渦流として集合させることにより、固形分から軽量異物類の分離機能が促進され上昇流による浮遊分離効率
が高まるとしている点である。
The point to be observed here is that the centrifugally-falling granular material-containing air flow is gathered as a vortex flow in which the flow velocity is suddenly increased by the partition plate having the opening in the center to the lower space portion of the tip opening of the air flow discharge pipe. In other words, the function of separating lightweight foreign substances from the solid content is promoted and the floating separation efficiency by the upward flow is increased.
 しかしながら、破砕処理後の廃棄プラスチック類は10mm以下を要請(許容)している点で粒度分布が乱雑であり嵩比重もまちまちであると推認される。要するに、破砕により生じた粒状固形分と、剥離した表面研削層(粉砕微粉)、紙片、テープ片その他の嵩比重の小さい軽量異物等をサイクロン型の気流を応用して浮遊選別するものであろうと思われる。 However, it is presumed that the discarded plastics after the crushing treatment are requested (allowed) to be 10 mm or less, the particle size distribution is messy and the bulk specific gravity varies. In short, the granular solids generated by crushing and the separated surface grinding layer (pulverized fine powder), paper pieces, tape pieces, and other light foreign matters with small bulk specific gravity, etc. will be floated and sorted using a cyclone type air flow. Seem.
 一方、使用済のブラスト材(本発明の研削材に相当)を分離回収する提案も幾つか知られている(例えば、特許文献2、3、4及び5を参照)。これら従来例は、概してフィルター分離、篩選別、風選選別又は浮遊選別である。 On the other hand, some proposals for separating and collecting used blasting material (corresponding to the grinding material of the present invention) are also known (see, for example, Patent Documents 2, 3, 4, and 5). These conventional examples are generally filter separation, sieve sorting, wind sorting or floating sorting.
特開2004-283720号公報JP 2004-283720 A 特開2004-9222号公報JP 2004-9222 A 特開2001-212764号公報Japanese Patent Laid-Open No. 2001-212764 特開平9-193019号公報JP-A-9-193019 特開平8-25223号公報JP-A-8-25223
 近年、ブラスト用の非金属系研削材として、天然鉱物のうち「けい砂」は珪肺症予防の観点から使用しないので、アルマンディンガーネット[Fe3Al2(SiO4)3] の代替使用が増大している。代表的な物性のうち比重は4.1 、モース硬度は 7.6-8.3 である。なお、ガーネットはほどんど輸入に頼っているのが現状である。 In recent years, as a non-metallic abrasive for blasting, "silica sand" is not used from the viewpoint of silicosis as a natural mineral, so the use of Almandingernet [Fe 3 Al 2 (SiO 4 ) 3 ] has increased. is doing. Among the typical physical properties, the specific gravity is 4.1 and the Mohs hardness is 7.6-8.3. Garnet currently relies heavily on imports.
 例えば、ブラスト工程を経たガーネット粉粒体(被処理混合物)の性状は、粒度分布(粒径)でいえば、概略3mm以下である。そして、研削材として再使用可能なガーネット粉粒体(減耗後)が仮に0.2mm以上であるとすると、0.2mm未満、より具体的には0.1mm未満の粉体は表面剥離した(研掃された)塗膜や錆などの軽量異物類と磨耗により生じた研削粉からなる廃棄処理されてよい粉体(以下、産廃粉体)である。この種の研削材について、現状では、ブラスト工程を経たあとは廃棄処分している。 For example, the property of the garnet powder (mixture to be treated) that has undergone the blasting process is approximately 3 mm or less in terms of the particle size distribution (particle size). Then, assuming that the garnet powder that can be reused as an abrasive (after depletion) is 0.2 mm or more, the surface of the powder of less than 0.2 mm, more specifically less than 0.1 mm peeled ( It is a powder (hereinafter referred to as industrial waste powder) that can be disposed of, consisting of lightweight foreign substances such as a coated film or rust and grinding powder generated by wear. Currently, this type of abrasive is discarded after the blasting process.
 こうしたなかで、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物、とりわけ、乾式エアーブラスト装置によるブラスト工程を経た粉粒体(これに同伴される軽量異物類を含む)を効率よく分離し、再使用可能な粉粒体(以下、リサイクル可能粒体)を回収することによりマテリアルリサイクルを推進することが強く望まれている。この種の被処理混合物は比重差が比較的小さく、これを分離処理するという問題もある。 Among them, a mixture to be treated in which a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less, and light-weight foreign substances accompanied therewith, in particular, Efficiently separate powder (including lightweight foreign substances accompanying it) that has undergone a blasting process using a dry air blasting device, and collect reusable powder (hereinafter recyclable granules) Therefore, it is strongly desired to promote material recycling. This kind of mixture to be treated has a relatively small difference in specific gravity, and there is also a problem that this is separated.
 しかしながら、上記従来技術を適用しようとしても、比重差の小さいもの同士の分離は困難で、再使用可能な粒径(例えば0.2~0.5mm程度)の粉粒体(研削材)が廃棄側に移行してしまうか、回収側に産廃粉体(例えば0.2mm未満)がかなり残留してしまうという問題があった。しかも、従来技術はバッチ処理であると推認され、ブラスト作業の現場と分離処理の現場との間の移送の問題がある。 However, even if the above-mentioned conventional technology is applied, it is difficult to separate those having a small specific gravity difference, and a reusable powder (abrasive) having a particle size (for example, about 0.2 to 0.5 mm) is discarded. There is a problem that the waste powder (for example, less than 0.2 mm) remains considerably on the recovery side. Moreover, it is assumed that the prior art is batch processing, and there is a problem of transfer between the site of blasting operation and the site of separation processing.
 当然のことながら、ブラスト作業の現場でブラスト工程を経た粉粒体(詳しくは被処理混合物)に対して分離処理をおこない、直ちに再使用に供するようにしたいという課題提起があった。しかも、研削材回収の歩留りを高めたいという要請から、分離精度を改善するという課題もある。 As a matter of course, there has been a problem that it is desired to perform a separation process on a granular material (specifically, a mixture to be treated) that has undergone a blasting process at the site of blasting work and to immediately reuse it. In addition, there is also a problem of improving the separation accuracy in response to a request to increase the yield of abrasive recovery.
 本発明者らは、この種の粉粒体(これに同伴される軽量異物類を含む被処理混合物)を、研削材として再使用可能なリサイクル可能粒体と産廃粉体とに分離し、リサイクル可能粒体を効率的に回収可能な分離処理技術の研究開発を進めてきた。 The present inventors have separated and recycled this type of granular material (a mixture to be treated including light-weight foreign substances accompanying it) into recyclable granular material and industrial waste powder that can be reused as an abrasive. We have been researching and developing separation technology that can efficiently recover possible particles.
 特に、既存の集塵装置や電気掃除機等の外部吸引機器の前流に粉粒体分離処理装置を配置して接続し、該粉粒体分離処理装置によりリサイクル可能粒体を系内回収し、産廃粉体を系外排出して外部吸引機器の負荷を低減する試みを重ねてきた。 In particular, a granular material separation processing device is arranged and connected in the upstream of an external suction device such as an existing dust collector or vacuum cleaner, and the recyclable granular material is recovered in the system by the granular material separation processing device. Attempts have been made to reduce the load on external suction equipment by discharging industrial waste powder out of the system.
 第1の基礎出願に係る本発明(粉粒体分離処理装置及び粉粒体分離処理方法)は、その成果物のひとつであって、新たな装置構成により、分離処理容器内に受け入れた被処理混合物を、該容器内で流動を制御しながら気流と比重差を利用して多段的に産廃粉体を吸引排出するとともにリサイクル可能粒体を落下回収する手法で分離処理するものである。 The present invention (powder body separation processing apparatus and powder body separation processing method) according to the first basic application is one of the deliverables, and the processing object received in the separation processing container by a new apparatus configuration The mixture is separated and processed by suctioning and discharging the industrial waste powder in a multistage manner using the air flow and the difference in specific gravity while controlling the flow in the container and dropping and collecting the recyclable particles.
 また、継続的な研究開発を推進するなかで、本発明者の一人〔徳田智昭〕は、第1の基礎出願に係る粉粒体分離処理装置、その前・後流機器(装置)及び附属機器からなる装置系ユニットを構成し、被処理混合物を受入れて(系内導入し)、リサイクル可能粒体と軽量異物類を含む産廃粉体の分離処理からそれらの分別回収までの一連の工程処理を系統的に系内処理可能とするコンパクトな分離回収処理システムを構想してきた。 In addition, while promoting continuous research and development, one of the present inventors [Tomoaki Tokuda], the granular material separation treatment apparatus, the front / rear-stream equipment (apparatus) and associated equipment according to the first basic application. A system unit consisting of the above, accepts the mixture to be treated (introduced into the system), and performs a series of processing from separation processing of industrial waste powder containing recyclable granules and lightweight foreign substances to separation and collection of them We have envisioned a compact separation and recovery processing system that enables systematic processing in the system.
 第2の基礎出願に係る本発明(粉粒体分離回収処理システム)はその成果物のひとつであって、単一のプラットフォーム上に、第1の基礎出願に係る本発明装置(粉粒体分離処理装置)を包含する装置系ユニットを搭載してコンパクト化し、可搬的で機動的な粉粒体分離回収処理システムを開発するに至ったものである。 The present invention (powder particle separation and recovery processing system) according to the second basic application is one of the products, and the present invention device (powder particle separation) according to the first basic application on a single platform. It has been compacted by mounting a system unit including a processing apparatus), and has led to the development of a portable and agile granular material separation and recovery processing system.
 第1の基礎出願に係る本発明が解決しようとする問題点は、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を分離し、リサイクル可能粒体を系内回収する点にある。ここに、粉粒体と軽量異物類との比重差は比較的小さいという点を考慮する必要がある。 The problem to be solved by the present invention relating to the first basic application is that the specific gravity and hardness are relatively large and the particle size is a grit-like or shot-like initial shape having a particle size of several millimeters or less, and the accompanying particles. It is the point which isolate | separates the to-be-processed mixture in which the lightweight foreign materials mixed are collected, and collect | recovers recyclable granule in a system. Here, it is necessary to consider that the specific gravity difference between the granular material and the lightweight foreign substances is relatively small.
 とりわけ、乾式エアーブラスト装置によるブラスト工程を経た研削材からなる粉粒体(これに同伴される軽量異物類を含む)を分離し、リサイクル可能粒体を系内回収するとともに、軽量異物類や粒径の小さい産廃粉体を系外排出する点を技術解決課題とする。これにより、マテリアルリサイクルを推進するという目的効果の達成を図る。あわせて、後流接続した外部吸引機器の負荷を低減するという目的効果も包含する。 In particular, powder particles (including lightweight foreign substances accompanying them) that have been subjected to a blasting process using a dry air blasting device are separated, and recyclable particles are collected in the system. The technical solution is to discharge small-sized industrial waste powder out of the system. This will achieve the objective effect of promoting material recycling. In addition, it also includes the objective effect of reducing the load on the external suction device connected downstream.
 第1の基礎出願に係る本発明はこのような事情に鑑みてなされたものであり、上記課題を解消し、集塵装置や電気掃除機等の外部吸引機器に接続した分離処理容器に被処理混合物を吸引導入し、該容器内で流動を制御しながら乾式で気流と比重差を利用して分離処理し、粉粒体(リサイクル可能粒体)を系内回収するとともに、産廃粉体を含む軽量異物類を外部吸引機器に向けて系外排出するための粉粒体分離処理装置及び粉粒体分離処理方法を提供するものである。 The present invention according to the first basic application has been made in view of such circumstances, and solves the above-described problems, and is processed in a separation processing container connected to an external suction device such as a dust collector or a vacuum cleaner. The mixture is sucked in and separated while utilizing the air flow and the specific gravity difference while controlling the flow in the container, and the granular material (recyclable granular material) is recovered in the system and contains the industrial waste powder. The present invention provides a granular material separation processing apparatus and a granular material separation processing method for discharging lightweight foreign substances out of the system toward an external suction device.
 一方、第2の基礎出願に係る本発明が解決しようとする問題点は、第1の基礎出願に係る粉粒体分離処理装置と、該装置にバキューム接続する前・後流の連係機器(装置)を装置系ユニットとして処理系統を機能構成し、一の装置系内でリサクル可能粒体と軽量異物類を含む産廃粉体を分離し、かつ、分別して回収する一連の系統的な処理をおこなう点にある。 On the other hand, the problem to be solved by the present invention related to the second basic application is that the granular material separation processing apparatus according to the first basic application and the upstream and downstream linked devices (apparatuses) vacuum connected to the apparatus. ) As a system unit, and a series of systematic processing to separate and collect the reusable particles and industrial waste powder containing lightweight foreign substances in one system. In the point.
 また、装置系ユニットをプラットフォームとなる単一の枠体(後述の可搬性機枠)内に搭載(収設)し、かつ、工程順にライン配置して処理系統を機能構成し、輸送可能で現場設置可能な機動性をもたせるという点もある。 In addition, the equipment unit is mounted (collected) in a single frame (portable machine frame, which will be described later) as a platform, and the processing system is functionally configured by arranging the lines in the order of the processes. There is also the point of having mobility that can be installed.
 第2の基礎出願に係る本発明はこのような事情に鑑みてなされたものであり、上記課題を解消し、装置系ユニットを作業現場(例えば、乾式エアーブラスト装置)にアクセス可能に設置し、作業で発生する被処理混合物(例えば、ブラスト後の研削材)を吸引導入し、分離から回収までの一連の系統的な処理をおこなうようにした粉粒体分離回収処理システムを提供するものである。 The present invention according to the second basic application is made in view of such circumstances, solves the above problems, and installs an apparatus unit so as to be accessible to a work site (for example, a dry air blast apparatus), The present invention provides a granular material separation and recovery processing system in which a mixture to be processed (for example, abrasive after blasting) generated by work is sucked in and a series of systematic processing from separation to recovery is performed. .
 課題を解決するために第1の基礎出願に係る本発明は、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を系内導入し、乾式で前記粉粒体と前記軽量異物類とを分離処理する粉粒体分離処理装置において、
集塵装置や電気掃除機等の外部吸引機器に接続した分離処理容器に前記被処理混合物を吸引導入し、該容器内で流動を制御しながら気流と比重差を利用して分離処理し、前記粉粒体を系内回収するとともに、前記軽量異物類を前記外部吸引機器に向けて系外排出するための粉粒体分離処理装置であって、
前記粉粒体を回収貯留するホッパタンクと、該ホッパタンクの上部構造として被冠封着され周面に前記被処理混合物を受け入れる吸引導入管と、上面に前記外部吸引機器に接続する吸引排出管を設けた分離処理容器を備えるとともに、
前記分離処理容器が、漏斗状に底面形成した分離コーンと、該分離コーンの先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口を有してなり、
前記吸引排出管が、その先端部を多重管構成とし、それぞれの軸芯を前記分離コーンの回転軸(円錐軸)に合致させ、かつ、それらの管径を前記筒口の各口径に対応する小径なものとして遊挿して開口端部に臨ませてなり、
前記分離処理容器内に吸引導入した前記被処理混合物を前記筒口に向けて落下誘導するとともに、前記吸引排出管により軽量異物類を多段階に吸引して系外排出し、残る粉粒体を系内に落下回収するようにしたことを特徴とするものである。
In order to solve the problem, the present invention according to the first basic application is accompanied by a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less, and this. In the granular material separation processing apparatus that introduces the mixture to be treated mixed with the lightweight foreign substances into the system and separates the powder and the lightweight foreign substances by a dry process,
The mixture to be treated is sucked and introduced into a separation processing container connected to an external suction device such as a dust collector or a vacuum cleaner, and is separated using an air flow and a specific gravity difference while controlling flow in the container, A powder separation processing device for collecting powder particles in the system and discharging the lightweight foreign substances out of the system toward the external suction device,
A hopper tank that collects and stores the granular material, a suction introduction pipe that is crown-sealed as an upper structure of the hopper tank and receives the mixture to be treated on a peripheral surface, and a suction discharge pipe that is connected to the external suction device on the upper surface A separate processing container,
The separation processing container has a separation cone formed in a funnel-shaped bottom surface, and a cylindrical mouth that hangs downwardly from the tip of the separation cone and has a multi-stage formed by reducing its diameter stepwise.
The suction / discharge pipe has a multi-tube configuration at its tip, and each axis is aligned with the rotation axis (conical axis) of the separation cone, and the pipe diameter is a small diameter corresponding to each diameter of the tube opening It is loosely inserted as a thing and it faces the opening end,
The mixture to be treated sucked and introduced into the separation processing container is guided to drop toward the tube port, and light foreign matters are sucked in multiple stages by the suction and discharge pipe and discharged out of the system, and the remaining powder particles are discharged into the system. It is characterized by being dropped and collected inside.
 また、上記構成の粉粒体分離処理装置において、分離処理容器内で分離コーンによる被処理混合物の落下誘導と吸引排出管による軽量異物類の吸引排出とを協働させて流動を制御しながら粉粒体と軽量異物類とを分離処理するようにした粉粒体分離処理方法であって、
吸引導入により受け入れた前記被処理混合物を前記分離処理容器内で発生する気流を利用して軽重分離しながら、前記分離コーンの内表面に受け止めて旋回と落下を一旦阻止し、跳ね返りを含む爾後の自由落下に任せ、前記分離コーンの筒口に向けてカスケード状に落下誘導しながら、前記吸引排出管により軽量異物類を多段階に吸引して系外排出し、残る粉粒体を落下回収するようにしたことを特徴とするものである。
Further, in the granular material separation processing apparatus having the above-described configuration, the powder is controlled while controlling the flow by cooperating the drop induction of the mixture to be processed by the separation cone and the suction and discharge of the light foreign matters by the suction and discharge pipe in the separation processing container. It is a granular material separation processing method that separates granular materials and lightweight foreign substances,
While lightly separating the mixture to be treated received by introduction of suction using an air flow generated in the separation processing container, it is received on the inner surface of the separation cone to temporarily stop swirling and falling, and includes rebounding While letting it fall freely, inducing a drop in a cascade toward the cylinder mouth of the separation cone, lightweight foreign substances are sucked out in multiple stages by the suction / discharge pipe and discharged out of the system, and the remaining granular material is dropped and collected It is characterized by that.
 課題を解決するために第2の基礎出願に係る本発明は、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を吸引導入し、乾式で前記粉粒体と前記軽量異物類とを分離処理する粉粒体分離処理装置(第1の基礎出願に係る本発明装置に同じ)を包含し、該粉粒体分離処理装置にバキューム接続する前・後流の連係機器又は連係装置をプラットフォームとなる単一の枠体内に収設し、かつ、工程順にライン配置して系統的な処理をおこなうようにした粉粒体分離回収処理システムであって、
系外より被処理混合物を受け入れて一時貯留するための第1の工程処理を担当するホッパタンク装置と、
前記ホッパタンク装置から移送導入され、乾式で前記被処理混合物を構成する比較的粒径の大きいリサイクル可能粒体と比較的粒径の小さい産廃粉体及び軽量異物類とに分離処理するための第2の工程処理を担当する粉粒体分離処理装置と、
前記粉粒体分離処理装置の下段に脱着交換可能に設置され、分離処理後のリサイクル可能粒体を落下回収して貯留するための柔軟性袋体容器と、
前記粉粒体分離処理装置から配管導入され、分離処理後の廃棄粉体及び軽量異物類と粉塵とを分別処理するための第3の工程処理を担当する集塵サイクロン装置と、
前記集塵サイクロン装置の下段に脱着交換可能に設置され、分別処理後の前記産廃粉体及び軽量異物類を落下回収して貯留するための柔軟性袋体容器と、
前記集塵サイクロン装置と配管接続され、装置系のバキューム経路の駆動源となるとともに、分別処理後の粉塵を吸引導入して最終的に捕捉するための第4の工程処理を担当する電気掃除機その他の吸引装置と、
前記柔軟性袋体容器を含む装置群を工程順にライン配置して、単一のフレーム又はケーシング内に収設し、1ライン又は並列する複数ラインの処理系統からなる装置系ユニットを構設するとともに、輸送可能で現場設置可能なプラットフォームとして用いるための可搬性機枠を具備してなり
前記装置系ユニットを稼働させて前記第1乃至第4の工程処理を系統的に、かつ、系内で処理するようにしたことを特徴とするものである。
In order to solve the problem, the present invention according to the second basic application is accompanied by a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less, and this. A powder separation process apparatus for separating and processing the powder and the lightweight foreign substances in a dry manner by sucking and introducing the mixture to be treated with the light-weight foreign substances (into the apparatus of the present invention according to the first basic application) The same or the like, and the upstream and downstream linkage devices or linkage devices vacuum-connected to the granular material separation processing device are accommodated in a single frame as a platform, and the lines are arranged in the order of the processes. It is a granular material separation and recovery processing system that performs a typical process,
A hopper tank device in charge of the first process for receiving and temporarily storing the mixture to be treated from outside the system;
A second process for separating and processing into recyclable granules having a relatively large particle size, industrial waste powder and light-weight foreign matters having a relatively small particle size, which are transferred from the hopper tank apparatus and constitute the mixture to be treated in a dry manner. A granular material separation processing device in charge of the process of
A flexible bag container that is installed in the lower stage of the powder and particle separation apparatus so that it can be removed and replaced, and drops and collects the recyclable particles after the separation process,
A dust collecting cyclone apparatus in charge of a third process for separating and processing waste powder and light-weight foreign substances and dust after being piped from the granular material separation processing apparatus;
A flexible bag container that is installed in the lower stage of the dust collection cyclone device so as to be removable and replaceable, and that collects and collects the industrial waste powder and the lightweight foreign matters after the separation process, and
A vacuum cleaner connected to the dust collecting cyclone device and serving as a drive source for the vacuum path of the device system, and in charge of the fourth process for sucking and finally capturing the dust after the separation process With other suction devices,
The apparatus group including the flexible bag container is arranged in a line in the order of processes, and is arranged in a single frame or casing, and an apparatus system unit including a processing system of one line or a plurality of lines arranged in parallel is constructed. , Comprising a portable machine frame for use as a platform that can be transported and installed on-site, and operating the device system unit to systematically and process the first to fourth process steps It is characterized by doing so.
 第1の基礎出願に係る本発明装置によれば、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を分離処理し、粉粒体(リサイクル可能粒体)を系内回収し軽量異物類を含む産廃粉体を系外排出することができる。 According to the device of the present invention relating to the first basic application, a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less, and a light-weight foreign substance accompanying this The mixture to be treated can be separated, the granular material (recyclable granular material) can be recovered in the system, and the industrial waste powder containing lightweight foreign matters can be discharged out of the system.
 とりわけ、乾式エアーブラスト装置によるブラスト工程を経た研削材からなる粉粒体(これに同伴される軽量異物類を含む)を効率的に分離し、リサイクル可能粒体を系内回収することにより、マテリアルリサイクルの推進に寄与することができる。あわせて、産廃粉体(軽量異物類と減耗により粉体化した研削材を含む;以下同じ)を系外排出することにより、後流接続した外部吸引機器の負荷を低減することができる。 In particular, materials by efficiently separating powder particles (including lightweight foreign substances accompanying them) made of abrasives that have undergone a blasting process using a dry air blasting device and recovering recyclable particles in the system. It can contribute to the promotion of recycling. In addition, it is possible to reduce the load of the external suction device connected downstream by discharging industrial waste powder (including lightweight foreign substances and abrasive powdered by wear; the same applies hereinafter).
 また、第1の基礎出願に係る本発明方法によれば、分離コーンの筒口に向けてカスケード状の落下誘導と吸引排出を協働させて被処理混合物の流動を制御しながら多段的に粉粒体(リサイクル可能粒体)の系内回収と軽量異物等(産廃粉体)の系外排出が可能である。当然のことながら、被処理混合物の性状に応じて吸引力を最適調整可能とするものである。 In addition, according to the method of the present invention relating to the first basic application, the particles in a multistage manner are controlled while controlling the flow of the mixture to be processed by cooperating cascaded drop induction and suction discharge toward the tube opening of the separation cone. It is possible to recover the body (recyclable particles) in the system and discharge light foreign substances (industrial waste powder). Naturally, the suction force can be optimally adjusted according to the properties of the mixture to be treated.
  したがって、本発明方法の適用範囲は、研削材はもとより、廃プラスチック破砕粉粒体、穀類その他の粉粒体とこれに同伴する軽量異物類からなる種々の被処理混合物に及び、それぞれの分離条件に対して柔軟に対応可能で汎用性が高いという利点がある。 Therefore, the scope of application of the method of the present invention covers not only abrasives but also various plastic mixtures, such as waste plastic crushed powder, cereals and other powders, and light-weight foreign substances accompanying them. There is an advantage that it can respond flexibly and has high versatility.
 さらに、第2の基礎出願に係る本発明システムによれば、比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を系内導入し、リサイクル可能粒体と産廃粉体(軽量異物類を含む)の分離からリサイクル可能粒体と産廃粉体(軽量異物類を含む)の分別回収までの一連の工程処理を系統的におこなう装置系ユニットにより系内処理することができる。 Furthermore, according to the system of the present invention relating to the second basic application, a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less is accompanied by this. Introduce a mixture to be treated with a mixture of lightweight foreign substances and separate recyclable granules and industrial waste powder (including lightweight foreign substances) from recyclable granules and industrial waste powder (including lightweight foreign substances). In-system processing can be performed by an apparatus system unit that systematically performs a series of process processes up to fractional collection.
 とりわけ、装置系ユニットは可搬性機枠に搭載され輸送可能で現場設置可能なものとされるので、作業現場(例えば、乾式エアーブラスト装置)にアクセス可能に設置し、作業で発生する被処理混合物(例えば、ブラスト後の研削材)を吸引導入し、被処理混合物中
のリサイクル可能粒体と産廃粉体を効率的に分離し、該リサイクル可能粒体を系内回収することにより、マテリアルリサイクルの推進に寄与することができる。あわせて、産廃粉体を系外排出することなく分別回収することができる。
In particular, the equipment unit is mounted on a portable machine frame and can be transported and installed on-site, so that it can be installed at work sites (for example, dry air blasting equipment) and the mixture to be processed generated in the work. (For example, abrasive material after blasting) is sucked in, the recyclable granules and the industrial waste powder in the mixture to be treated are separated efficiently, and the recyclable granules are recovered in the system, so that material recycling Can contribute to the promotion. At the same time, industrial waste powder can be collected separately without being discharged out of the system.
実施例装置の斜視説明図である。It is a perspective explanatory view of an example device. 実施例装置の断面視説明図である。It is sectional drawing explanatory drawing of an Example apparatus. 図2中P部詳細説明図である。It is P section detailed explanatory drawing in FIG. 分離処理容器内での被処理混合物の流動制御を示す模式説明図である。It is a schematic explanatory drawing which shows the flow control of the to-be-processed mixture in a separation processing container. 実施例装置の性能(作用効果)に係る実験的事実を示す粒度分布に関するそれぞれの篩試験結果とそのデータプロットである。ここに、(a)はブラスト後未処理の被処理混合物(供試材)、(b)は分離処理後のリサイクル可能粒体、及び(c)は分離処理後の廃棄粉体についてのものである。It is each sieve test result regarding the particle size distribution which shows the experimental fact which concerns on the performance (effect) of an Example apparatus, and its data plot. Here, (a) is for the untreated mixture (test material) after blasting, (b) is for the recyclable granules after separation treatment, and (c) is for the waste powder after separation treatment. is there. 実施例装置とブラスト装置(前流)と外部吸引機器(後流)とで装置系を構成する場合の接続例を示す構成概要説明図である。It is a structure outline explanatory view showing the example of connection in the case where an apparatus system is constituted by an example device, a blast device (front flow), and an external suction device (back flow). 実施例システムの正面視構成概要説明図である。It is a front view composition outline explanatory view of an example system. 実施例システムの平面視構成概要説明図である。It is a planar view structure outline explanatory drawing of an Example system. 図7中、I-I矢視構成概要説明図である。FIG. 8 is a schematic explanatory diagram taken along the line II in FIG. 作業現場との接続例を示す実施例システムの構成概要説明図である。It is a structure outline explanatory drawing of the example system which shows the example of connection with a work site. 粉粒体分離処理装置の断面視説明図である。It is sectional view explanatory drawing of a granular material separation processing apparatus. 図11中、P部詳細説明図である。In FIG. 11, it is a P part detailed explanatory drawing.
  本発明を実施するための形態は、第1の基礎出願に係る上記構成の粉粒体分離処理装置において、分離コーンは、内表面に複数の弾性体からなる整流リブを放射形成したものとされる。 The mode for carrying out the present invention is the granular material separation processing apparatus having the above configuration according to the first basic application, wherein the separation cone is formed by radiating rectification ribs made of a plurality of elastic bodies on the inner surface. The
 ここで、被処理混合物は、至適には、乾式エアーブラスト装置によるブラスト工程を経たものである。金属系研削材か非金属系研削材かを問わない。 Here, the mixture to be treated is optimally subjected to a blasting process using a dry air blasting apparatus. It doesn't matter whether it is a metallic or non-metallic abrasive.
 また、第1の基礎出願に係る上記構成の粉粒体分離処理方法において、被処理混合物の落下誘導を増補するために、分離コーンの内表面に複数の弾性体からなる整流リブを放射形成して被処理混合物を受け止めるようにしている。 Moreover, in the granular material separation processing method of the above configuration according to the first basic application, in order to augment the fall induction of the mixture to be treated, rectifying ribs made of a plurality of elastic bodies are formed radially on the inner surface of the separation cone. The mixture to be treated.
  第2の基礎出願に係る上記構成の粉粒体分離回収処理システムにおいて、粉粒体分離処理装置は、第1の基礎出願に係る粉粒体分離処理装置を用いるものであってよい。 に お い て In the granular material separation and recovery processing system with the above configuration according to the second basic application, the granular material separation processing device may use the granular material separation processing device according to the first basic application.
 その特徴構成は、粉粒体を回収貯留するホッパタンク部と、該ホッパタンク部の上部構造として被冠封着され周面に被処理混合物を受け入れる吸引導入管と、上面に吸引機器に接続する吸引排出管を設けた分離処理容器を備えるとともに、該分離処理容器が、漏斗状に底面形成した分離コーンと、該分離コーンの先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口を有してなり、
前記吸引排出管が、その先端部を多重管構成とし、それぞれの軸芯を前記分離コーンの回転軸(円錐軸)に合致させ、かつ、それらの管径を前記筒口の各口径に対応する小径なものとして遊挿して開口端部に臨ませてなり、
前記分離処理容器内に吸引導入した前記被処理混合物を前記筒口に向けて落下誘導するとともに、前記吸引排出管により産廃粉体を多段階に吸引して後流の集塵サイクロン装置へ排出し、残る粉粒体を柔軟性袋体容器に落下回収するようにしたものとされる。
Its characteristic configuration is a hopper tank part for collecting and storing powder particles, a suction inlet pipe that is sealed as a top structure of the hopper tank part and receives the mixture to be treated on the peripheral surface, and a suction discharge connected to a suction device on the upper surface A separation processing container provided with a pipe, the separation processing container is formed in a funnel-shaped bottom surface with a separation cone and a downwardly projecting drop from the tip of the separation cone, and its diameter is reduced stepwise. It has a multi-stage formed tube mouth,
The suction / discharge pipe has a multi-tube configuration at its tip, and each axis is aligned with the rotation axis (conical axis) of the separation cone, and the pipe diameter is a small diameter corresponding to each diameter of the tube opening It is loosely inserted as a thing and it faces the opening end,
Inducing and dropping the treated mixture sucked and introduced into the separation processing container toward the cylinder port, the waste powder is sucked in multiple stages by the suction discharge pipe and discharged to a downstream dust collecting cyclone device, It is assumed that the remaining granular material is dropped and collected in the flexible bag container.
 ここで、被処理混合物は、至適には、乾式エアーブラスト装置によるブラスト工程を経
たもの(金属系研削材か非金属系研削材かを問わない)であり、直接又は一時貯留してホッパタンク装置に圧送供給されるものである。
Here, the mixture to be treated is optimally subjected to a blasting process using a dry air blasting device (whether metallic grinding material or non-metallic grinding material), and the hopper tank device is stored directly or temporarily. Is fed by pressure.
  第1の基礎出願に係る本発明の粉粒体分離処理装置の一実施例(以下、実施例装置X)を添付図面を参照して以下説明する。 実 施 An example (hereinafter referred to as Example device X) of the granular material separation processing device of the present invention according to the first basic application will be described below with reference to the accompanying drawings.
 図1に実施例装置Xの斜視説明図を示す。 FIG. 1 is a perspective explanatory view of the apparatus X of the embodiment.
 図示のとおり、実施例装置Xは、集塵装置や電気掃除機等の外部吸引機器〔図示省略〕に接続され、乾式エアーブラスト装置〔図示省略〕によるブラスト工程を経た系研削材からなる粉粒体と、これに同伴される軽量異物類からなる被処理混合物を分離処理容器1内に吸引導入し、乾式で気流と比重差を応用して分離処理し、粉粒体を系内回収するとともに、軽量異物類(産廃粉体を含む)を外部吸引機器に向けて系外排出するものである。 As shown in the figure, the embodiment apparatus X is connected to an external suction device (not shown) such as a dust collector or a vacuum cleaner, and is made of a system abrasive material that has undergone a blasting process by a dry air blast device (not shown). And the mixture to be treated, which is made of light foreign substances accompanying the body, is sucked into the separation processing container 1 and separated by applying the air flow and the difference in specific gravity in a dry manner to collect the granular material in the system. , Lightweight foreign matters (including industrial waste powder) are discharged out of the system toward an external suction device.
 分離処理容器1は、粉粒体を回収貯留するホッパタンク4と、該ホッパタンク4の上部構造として被冠封着されるものであり、周面に被処理混合物を受け入れる吸引導入管2と、上面に外部吸引機器に接続する吸引排出管3を備えている。なお、ホッパタンク4の下部には脱着自在な回収コンテナ41を配設している。 The separation processing container 1 is a hopper tank 4 for collecting and storing powder particles, a crown seal as an upper structure of the hopper tank 4, a suction introduction pipe 2 for receiving a mixture to be processed on the peripheral surface, and an upper surface A suction discharge pipe 3 connected to an external suction device is provided. A removable collection container 41 is disposed below the hopper tank 4.
 図2に実施例装置Xの断面視説明図、図3に図2中P部詳細説明図を示す。 FIG. 2 is a cross-sectional explanatory view of the embodiment apparatus X, and FIG.
 図示のとおり、分離処理容器1の内部構造は、その底面を漏斗状に形成した分離コーン11と、該分離コーン11の先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口13を有している。 As shown in the drawing, the internal structure of the separation processing container 1 has a separation cone 11 whose bottom surface is formed in a funnel shape, and hangs downward from the tip of the separation cone 11 in a convex manner, and its diameter is reduced stepwise. A cylindrical port 13 formed in multiple stages is provided.
 また、分離コーン11には、内表面に複数の弾性体からなる整流リブ12を放射形成している。 Also, the separation cone 11 is formed with radiation straightening ribs 12 made of a plurality of elastic bodies on the inner surface.
 吸引排出管3は、その先端部を多重管構成(31;31)とし、それぞれの軸芯を分離コーン11の回転軸(円錐軸)に合致させ、かつ、それらの管径を筒口13の各口径に対応する小径なものとして遊挿して開口端部に臨ませたものとしている。 The suction / discharge pipe 3 has a multi-tube structure (31; 31) at its tip, the axis of each is aligned with the rotation axis (conical axis) of the separation cone 11, and the diameter of each pipe is set to each of the tube ports 13. It is assumed that it is loosely inserted as a small diameter corresponding to the diameter and faced to the opening end.
  図4に分離処理容器内での被処理混合物の流動制御を模式的に説明する断面視模式説明図を示す。 FIG. 4 is a schematic explanatory view in cross section for schematically explaining the flow control of the mixture to be processed in the separation processing container.
 図3及び図4にそれぞれ示すように、分離処理容器1内に吸引導入した被処理混合物Mを筒口13に向けて落下誘導するとともに、吸引排出管3(31;31)により軽量異物類m2(産廃粉体を含む)を多段階に吸引して系外排出し、残る粉粒体m1(リサイクル可能粒体)を自由落下させて系内回収するようにしている。 As shown in FIGS. 3 and 4, the mixture to be treated M sucked and introduced into the separation processing container 1 is guided to drop toward the tube port 13, and light-weight foreign matter m2 (by the suction discharge pipe 3 (31; 31)). (Including industrial waste powder) is sucked out in multiple stages and discharged out of the system, and the remaining powder m1 (recyclable particles) is freely dropped and recovered in the system.
 より具体的には、被処理混合物Mを分離処理容器内で発生する気流を利用して軽重分離しながら、分離コーン11の内表面に受け止めて旋回と落下を一旦阻止し、跳ね返りを含む爾後の自由落下に任せ、筒口13に向けてカスケード状に落下誘導しながら、吸引排出管3(31;31)により軽量異物類m2(産廃粉体を含む)を多段階に吸引して系外排出し、残る粉粒体m1(リサイクル可能粒体)を落下回収するものである。 More specifically, the mixture to be treated M is lightly separated using an air flow generated in the separation processing vessel, and is received on the inner surface of the separation cone 11 to temporarily stop swirling and falling. While letting it fall freely, guiding the fall to the tube port 13 in a cascading manner, the suction discharge pipe 3 (31; 31) sucks lightweight foreign matter m2 (including industrial waste powder) in multiple stages and discharges it outside the system. The remaining granular material m1 (recyclable granular material) is dropped and collected.
 ここで、分離コーン11の内表面に複数の弾性体からなる整流リブ12を放射形成して被処理混合物M(m1;m2)を受け止めることにより、旋回方向への流動を阻止し、かつ、落下誘導を増補するものとしている。 Here, a flow straightening rib 12 made of a plurality of elastic bodies is formed on the inner surface of the separation cone 11 to receive the mixture to be processed M (m1; m2), thereby preventing the flow in the swirling direction and dropping. The guidance is to be augmented.
 以下、実験的事実の基づき実施例装置Xの作用効果を説明する。 Hereinafter, the operational effects of the embodiment apparatus X will be described based on experimental facts.
 供試材は、ブラスト後未処理のガーネット研削材(被処理混合物)であり、図5(a)は、その粒度分布(粒径)を示す篩試験(はかり取り)の結果とそのデータプロットである。 The specimen is an untreated garnet abrasive (mixture to be treated) after blasting, and FIG. 5 (a) is a result of a sieve test (weighing) showing its particle size distribution (particle size) and its data plot. is there.
 この図(篩試験結果)から理解されるように、被処理混合物の全量に対して0.2mm未満の粉粒体が61.8重量%を占めている。 As can be understood from this figure (result of the sieve test), the powder particles of less than 0.2 mm account for 61.8% by weight with respect to the total amount of the mixture to be treated.
 図5(b)は、分離処理後に系内回収された再使用可能な粉粒体(図中名称のリサイクル可能粒体に同じ)の粒度分布(粒径)を示す篩試験(はかり取り)の結果とそのデータプロットである。 FIG. 5 (b) shows a sieve test (weighing scale) showing the particle size distribution (particle size) of a reusable granular material (same as the recyclable granular material in the figure) recovered in the system after the separation treatment. The result and its data plot.
 この図(篩試験結果)から理解されるように、被処理混合物の全量に対する0.2mm未満の粉粒体の割合は44.6重量%を占めている。 As can be understood from this figure (results of the sieve test), the proportion of the granular material of less than 0.2 mm with respect to the total amount of the mixture to be treated accounts for 44.6% by weight.
 図5(c)は、分離処理後の系外排出された廃棄粉体(図中名称の産廃粉体に同じ)の粒度分布(粒径)を示す篩試験(はかり取り)の結果とそのデータプロットである。 FIG. 5 (c) shows the result of the sieve test (weighing scale) showing the particle size distribution (particle size) of the waste powder discharged from the system after separation (same as the industrial waste powder with the name in the figure) and its data. It is a plot.
 この図(篩試験結果)から理解されるように、被処理混合物の全量に対する0.2mm未満の粉粒体の割合は84.9重量%を占めている。 As can be understood from this figure (result of the sieve test), the proportion of the granular material of less than 0.2 mm with respect to the total amount of the mixture to be treated occupies 84.9% by weight.
 なお、分離処理後に系内回収されたリサイクル可能粒体と系外排出された廃棄粉体の割合は65:35であった。 In addition, the ratio of the recyclable granules collected in the system after the separation treatment and the waste powder discharged out of the system was 65:35.
 〔考察及び効果〕
 まず、ブラスト後未処理の被処理混合物において、リサイクル可能粒体(粒径0.2mm以上)と産廃粉体(粒径0.2mm未満)が占める割合は4:6程度である〔図5(a)参照〕。
[Discussion and effect]
First, the ratio of recyclable granules (particle size of 0.2 mm or more) and industrial waste powder (particle size of less than 0.2 mm) in the untreated mixture after blasting is about 4: 6 [FIG. see a)].
 そこで、この被処理混合物(ブラスト後未処理)に対して分離処理をおこなって、該被処理混合物全量の65重量%を系内回収している〔データの図示は省略〕。 Therefore, the treated mixture (untreated after blasting) is subjected to separation treatment, and 65% by weight of the total amount of the treated mixture is recovered in the system (data not shown).
 このうち0.2mm未満の粉粒体の割合は44.6重量%を占めているから〔図5(b)参照〕、残る55.4重量%(すなわち被処理混合物全量の3割程度)が再使用において全く問題なく有効利用可能な粉粒体であるといえる。 Of these, the proportion of particles less than 0.2 mm accounted for 44.6% by weight (see FIG. 5 (b)), and the remaining 55.4% by weight (that is, about 30% of the total amount of the mixture to be treated) It can be said that it is a granular material that can be effectively used without any problem in reuse.
 実際には、系内回収した65重量%のリサイクル可能粒体に、目減り分の35重量%相当のバージン材(研削材)を補充して再使用に供することになる。 Actually, virgin material (grinding material) equivalent to 35% by weight of the reduced amount is replenished to 65% by weight of recyclable particles collected in the system and used for reuse.
 なるほど、リサイクル可能粒体には0.2mm未満の粉粒体が混入しているので、再使用におけるブラスト作業では研削性能がやや劣るのではないかとの懸念があるかもしれない。 Indeed, since particles that are less than 0.2 mm are mixed in the recyclable particles, there may be a concern that the grinding performance may be slightly inferior in the blasting operation in reuse.
 しかしながら、微粒子も圧縮空気に載って研削対象表面に衝突するので、研削性能に大きく影響することはない。ただし、粉塵はやや増えることになる。 However, since the fine particles are also carried on the compressed air and collide with the surface to be ground, the grinding performance is not greatly affected. However, the dust will increase slightly.
 いずれにしても、バージン材でブラスト工程を経た被処理混合物について、その6割程度を再使用に供するという点で、このマテリアルリサイクルは従前にない大幅なコストダ
ウンに寄与するものである。
In any case, this material recycling contributes to an unprecedented significant cost reduction in that about 60% of the mixture to be treated that has undergone a blasting process with a virgin material is reused.
 もちろん、再使用に供されたブラスト後の研削材を被処理混合物として再度分離処理を施すことも考慮されてよい。 Of course, it may be considered that the blasted abrasive that has been reused is treated again as a mixture to be treated.
 当然のことながら、再処理の回数に応じて産廃粉体の割合が増大し、リサイクル可能粒体の系内回収率は低下するが、補充するバージン材(研削材)の割合を増やすことになるので、研削性能が大きく低下してゆく懸念はない。費用対効果を勘案すれば、再処理回数は数回に留めるの実際的である。 As a matter of course, the proportion of industrial waste powder increases with the number of reprocessing, and the recovery rate of recyclable granules decreases, but the proportion of virgin material (grinding material) to be supplemented increases. Therefore, there is no concern that the grinding performance will be greatly reduced. Considering the cost effectiveness, it is practical to keep the number of reprocessing only a few.
 一方、この被処理混合物(ブラスト後未処理)に対して分離処理をおこなって、該被処理混合物全量の35重量%を系外排出している〔データの図示は省略〕。 On the other hand, a separation process is performed on the mixture to be treated (untreated after blasting), and 35% by weight of the total amount of the mixture to be treated is discharged out of the system (data not shown).
 このうち、約6割は0.1mm未満の粉体であり、2割強が0.1mm以上0.2mm未満の粉体であり、総じて8割強(すなわち被処理混合物全量の3割程度)が産廃粉体である〔図5(c)参照〕。 Of these, about 60% are powders of less than 0.1 mm, and more than 20% are powders of 0.1 mm or more and less than 0.2 mm, and generally more than 80% (that is, about 30% of the total amount of the mixture to be treated). Is the industrial waste powder [see FIG. 5 (c)].
 したがって、系外排出される被処理混合物の8割強が廃棄粉体であり、これを受け入れる後流の集塵装置では無理な負荷をかけることなく塵埃処理を実行できる。 Therefore, over 80% of the mixture to be treated discharged out of the system is waste powder, and dust treatment can be carried out without imposing an excessive load on the downstream dust collector that accepts this.
 なお、残る2割弱は廃棄側(産廃粉体)に混入したリサイクル可能粒体(粒径0.2mm以上)であり、廃棄処分を余儀なくすることになるが、現在のところ、本発明手法による分離精度の許容限界である。 The remaining 20% is recyclable particles (particle size of 0.2 mm or more) mixed on the disposal side (industrial waste powder), which necessitates disposal. This is the allowable limit of separation accuracy.
 図6は実施例装置Xとブラスト装置(前流)と外部吸引機器(後流)とで処理系統を構成する場合の接続例を示す構成概要説明図である。 FIG. 6 is a schematic configuration explanatory diagram showing a connection example in the case where a processing system is configured by the embodiment device X, the blast device (front flow), and the external suction device (back flow).
 図6から理解されるように、実施例装置Xの前流に乾式エアーブラスト装置5を接続し、後流に集塵装置6、該集塵装置6に電気掃除機7を接続している。 As can be understood from FIG. 6, the dry air blast device 5 is connected to the upstream of the embodiment device X, the dust collector 6 is connected to the downstream, and the vacuum cleaner 7 is connected to the dust collector 6.
 ここで、乾式エアーブラスト装置5に代替して床面スイーパ51又は吸い口(ホースアタッチメント)52を接続する場合がある。吸引導入から吸引排出に至る管路系(容器内を含む)は電気掃除機7のバキューム機能を駆動源とする吸引経路である。 Here, instead of the dry air blast device 5, a floor surface sweeper 51 or a mouthpiece (hose attachment) 52 may be connected. A pipe line system (including the inside of the container) from suction introduction to suction discharge is a suction path using the vacuum function of the vacuum cleaner 7 as a drive source.
 このように、ブラスト作業に係る各機器を現場配置して連係接続するので、作業性が向上し、しかもマテリアルリサイクルによりコストダウンが可能となるものである。 In this way, since each device related to blasting work is placed on site and linked and connected, workability is improved and cost reduction is possible through material recycling.
  第2の基礎出願に係る本発明の一実施例である粉粒体分離回収処理システム(以下、実施例システムZ)を添付図面を参照して以下説明する。 粉 A granular material separation and recovery system (hereinafter referred to as Example System Z) which is an embodiment of the present invention relating to the second basic application will be described below with reference to the accompanying drawings.
 図7に正面視構成概要説明図、図8に平面視構成概要説明図及び図9に図7中I-I矢視構成概要説明図を示す。 7 is a front view configuration outline explanatory diagram, FIG. 8 is a plan view configuration overview explanatory diagram, and FIG. 9 is an II arrow configuration overview explanatory diagram in FIG.
 また、図10に作業現場との接続例を示す実施例システムZの構成概要説明図を示す。 In addition, FIG. 10 shows a schematic configuration diagram of an example system Z showing an example of connection with a work site.
 図示するように、実施例システムZは、乾式エアーブラスト装置5〔図10参照〕によるブラスト工程を経た研削材からなる粉粒体と、これに同伴される軽量異物類からなる被処理混合物を吸引導入し、乾式で粉粒体と産廃粉体とを分離処理する粉粒体分離処理装置X〔後述の図11参照〕を包含し、該粉粒体分離処理装置Xにバキューム接続する前・後流の
連係機器又は連係装置(8-6-7)をプラットフォームとなる単一の枠体内に収設し、かつ、工程順にライン配置して系統的な処理をおこなうようにしたものである。
As shown in the drawing, the embodiment system Z sucks a mixture made of abrasives that have undergone a blasting process by a dry air blasting device 5 [see FIG. Before and after the powder separation processing device X (see FIG. 11 to be described later) is introduced and vacuum-connected to the powder separation processing device X. The flow linkage device or linkage device (8-6-7) is housed in a single frame as a platform, and is arranged in a line in the order of processes for systematic processing.
 ホッパタンク装置8は、系外より被処理混合物〔図示では乾式エアーブラスト装置によるブラスト工程を経たもの〕を受け入れて一時貯留するための第1の工程処理を担当する。被処理混合物が系外より圧送される場合は、バグフィルタ81を介して脱気しながら受け入れることになる。 The hopper tank device 8 is in charge of a first process for receiving and temporarily storing a mixture to be treated (in the figure, a blast process by a dry air blast apparatus) from outside the system. When the mixture to be treated is pumped from outside the system, it is received while degassing through the bag filter 81.
 粉粒体分離処理装置X(実施例1記載の実施例装置Xに同じ)は、ホッパタンク装置8からスクリューフィーダ82を介して移送導入され、乾式で被処理混合物を構成する比較的粒径の大きいリサイクル可能粒体m1と比較的粒径の小さい産廃粉体m2とに分離処理するための第2の工程処理を担当する〔装置構成の詳細については後述〕。その下段には、分離処理後のリサイクル可能粒体を落下回収して貯留するための脱着交換可能な柔軟性袋体容器4a(以下、フレコンバック)を設置している。 The granular material separation treatment apparatus X (same as the embodiment apparatus X described in the embodiment 1) is transferred and introduced from the hopper tank apparatus 8 through the screw feeder 82, and has a relatively large particle size that constitutes the mixture to be treated in a dry type. Responsible for the second process for separating the recyclable particles m1 and the industrial waste powder m2 having a relatively small particle size (details of the apparatus configuration will be described later). In the lower stage, a detachable and replaceable flexible bag container 4a (hereinafter referred to as a flexible container bag) for dropping and collecting and storing the recyclable granules after separation is installed.
 集塵サイクロン装置6は、粉粒体分離処理装置Xから配管導入され、分離処理後の廃棄粉体と粉塵とを分別処理するための第3の工程処理を担当する。その下段には、分別処理後の産廃粉体m2を落下回収して貯留するための脱着交換可能なフレコンバック4bを設置している。 The dust collecting cyclone device 6 is introduced from the granular material separation processing device X by piping, and is in charge of the third process for separating the waste powder and dust after the separation processing. In the lower stage, a flexible container bag 4b that can be attached and detached is installed to drop and collect the industrial waste powder m2 after the separation process.
 電気掃除機その他の吸引装置7は、集塵サイクロン装置6と配管接続され、装置系のバキューム経路の駆動源となるとともに、分別処理後の粉塵を吸引導入して最終的に捕捉するための第4の工程処理を担当する。 The vacuum cleaner or other suction device 7 is connected to the dust collecting cyclone device 6 as a pipe and serves as a drive source for the vacuum path of the device system. In addition, the vacuum cleaner or other suction device 7 sucks and introduces the dust after the separation process and finally captures it. 4 process processing.
 可搬性機枠9は、フレコンバック4を含む装置群(8-X-6-7)を工程順にライン配置して、単一のフレーム又はケーシング内に収設し、1ライン又は並列する複数ラインの処理系統からなる装置系ユニットを構設するとともに、輸送可能で現場設置可能なプラットフォームとして用いるものである。図示の装置系ユニットの態様は並列的な2ラインを示している〔図8及び図10〕。 The portable machine frame 9 has a group of devices (8-X-6-7) including the flexible container bag 4 arranged in the order of the process, and is placed in a single frame or casing, and one line or a plurality of lines arranged in parallel. In addition to constructing a system unit consisting of the above processing systems, it is used as a platform that can be transported and installed on the site. The mode of the system unit shown in the figure shows two lines in parallel [FIGS. 8 and 10].
 そして、装置系ユニットを機器的に運用するコンパクトな処理システムを構築し、第1乃至第4の工程処理を系統化し、かつ、系内処理するようにしている。 Then, a compact processing system for operating the apparatus system unit in an apparatus is constructed, and the first to fourth process processes are organized and processed in the system.
  上記第2の工程処理を担当する粉粒体分離処理装置X(実施例1記載の実施例装置Xに同じ)に関し、図11に断面視説明図及び図12に図11中P部詳細説明図を示す。 FIG. 11 is a cross-sectional view of FIG. 11 and FIG. 12 is a detailed view of a portion P in FIG. 11 with respect to the granular material separation processing device X (same as Example device X described in Example 1) in charge of the second process. Indicates.
 図示のとおり、粉粒体分離処理装置Xは、リサイクル可能粒体m1を回収貯留するフレコンバック4と、該フレコンバック4aの上部構造として配置され周面に被処理混合物Mを受け入れる吸引導入管2と、上面に集塵サイクロン装置に接続する吸引排出管3を設けた分離処理容器1を備えている。 As shown in the figure, the granular material separation processing apparatus X includes a flexible container bag 4 that collects and stores recyclable granular material m1, and a suction introduction pipe 2 that is disposed as an upper structure of the flexible container bag 4a and receives the mixture to be processed M on its peripheral surface. And a separation processing container 1 provided with a suction / discharge pipe 3 connected to the dust collecting cyclone device on the upper surface.
 ここで、分離処理容器1の具体的構造は、漏斗状に底面形成した分離コーン11と、該分離コーン11の先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口13を有している。分離コーン11には、内表面に複数の弾性体からなる整流リブ12を放射形成している。 Here, the specific structure of the separation processing container 1 is a separation cone 11 formed in a funnel-shaped bottom, and is formed in a multi-stage structure by dropping downward from the tip of the separation cone 11 in a stepwise manner and reducing its diameter stepwise. It has the cylinder port 13 made. The separation cone 11 is radially formed with rectifying ribs 12 made of a plurality of elastic bodies on the inner surface.
 また、吸引排出管3は、その先端部を多重管構成とし、それぞれの軸芯を分離コーン11の回転軸(円錐軸)に合致させ、かつ、それらの管径を筒口13の各口径に対応する小径なものとして遊挿して開口端部に臨ませた構成とされる。 In addition, the suction / discharge pipe 3 has a multi-tube configuration at its tip, and the respective shaft cores are aligned with the rotation axis (conical axis) of the separation cone 11, and their pipe diameters correspond to the respective diameters of the tube port 13. It is set as the structure which loosely inserted as a small diameter thing to face, and faced the opening edge part.
 そして、分離処理容器1内に吸引導入した被処理混合物Mを筒口13に向けて落下誘導するとともに、吸引排出管3により産廃粉体m2を多段階に吸引して後流の集塵サイクロン装置6へ排出し、残るリサイクル可能粒体m1をフレコンバック4aに落下回収するようにしている。 The mixture to be treated M sucked and introduced into the separation processing container 1 is guided to drop toward the cylinder port 13 and the waste powder m2 is sucked in multiple stages by the suction / discharge pipe 3 to wake the dust collecting cyclone device 6 in the downstream. The remaining recyclable particles m1 are dropped and collected in the flexible container bag 4a.
 第1の基礎出願に係る本発明(粉粒体分離処理装置及び粉粒体分離処理方法)は、既存の外部吸引機器と連係(接続)することにより、分離処理容器内で、カスケード状の落下誘導と吸引排出を協働させて被処理混合物の流動を制御しながら、軽量異物類(産廃粉体)を多段的に排出可能とし、リサイクル可能粒体を系内回収可能とする点で、比重差が小さい粉粒体と軽量異物類からなる被処理混合物について分離精度を増補する革新的な手法を提案するものである。 The present invention (powder and particle separation processing apparatus and powder and particle separation processing method) according to the first basic application is linked (connected) to an existing external suction device, so that a cascade-like drop occurs in the separation processing container. Specific gravity in that lightweight foreign substances (industrial waste powder) can be discharged in multiple stages and recyclable granules can be recovered in the system while controlling the flow of the mixture to be treated by cooperating induction and suction discharge. The present invention proposes an innovative method for increasing the separation accuracy of a mixture to be treated consisting of a powder and a small amount of foreign substances having a small difference.
 第2の基礎出願に係る本発明(粉粒体分離回収処理システム)は、ブラスト作業に係るブラスト工程を経た研削材(被処理混合物)の工程処理を担当する各機器(装置)からなる装置系ユニットを構成し、かつ、輸送可能で現場設置可能な可搬性機枠に搭載することにより、一の装置系内でリサイクル可能粒体と産廃粉体の分離から分別回収までの一連の工程処理を系統的におこなうようにしており、機動的でコンパクトな粉粒体分離回収処理システムとして有用性が高いものである。 The present invention (powder body separation and recovery processing system) according to the second basic application is an apparatus system comprising devices (apparatuses) in charge of process processing of an abrasive (mixture to be processed) that has undergone a blasting process related to blasting By constructing the unit and mounting it on a portable machine frame that can be transported and installed on-site, a series of processes from separation to separation and collection of recyclable granules and industrial waste powder can be performed within one system. It is performed systematically, and is highly useful as a flexible and compact granular material separation and recovery treatment system.
 本発明のいずれにおいても、とりわけ乾式エアーブラスト装置のブラスト工程を経た研削材を被処理混合物として分離回収する際に、作業性が向上するとともに、マテリアルリサイクルによるコストダウンを推進する点で有用であり、斯界において貢献が期待できる。 In any of the present inventions, it is particularly useful in improving workability and promoting cost reduction by material recycling when separating and recovering abrasives that have undergone the blasting process of a dry air blasting apparatus as a mixture to be treated. A contribution can be expected in this field.
 1 分離処理容器
 11 分離コーン
  12 整流リブ
  13 筒口
 2 吸引導入管
  3 吸引排出管
  31 多重管
  4 ホッパタンク
  41 回収コンテナ
  5 乾式エアーブラスト装置
 51 床面スイーパ
  52 吸い口(ホースアタッチメント)
  6 集塵機(集塵サイクロン装置)
  7 電気掃除機(吸引装置)
  M 被処理物混合物
  m1 リサイクル可能粒体(再使用可能な研削材)
  m2 産廃粉体(軽量異物類及び減耗により粉体化した研削材を含む)
  X 粉粒体分離処理装置(実施例装置)

  4a 柔軟性袋体容器(フレコンバック)
  4b 柔軟性袋体容器(フレコンバック)
 8 ホッパタンク装置
 81 バグフィルタ
 82 スクリューフィーダ
 9 可搬性機枠(プラットフォーム)
 Z 粉粒体分離回収処理システム(実施例システム)
DESCRIPTION OF SYMBOLS 1 Separation processing container 11 Separation cone 12 Rectification rib 13 Cylinder port 2 Suction introduction pipe 3 Suction discharge pipe 31 Multiple pipe 4 Hopper tank 41 Collection container 5 Dry type air blasting device 51 Floor sweeper 52 Suction port (hose attachment)
6 Dust collector (dust collection cyclone device)
7 Vacuum cleaner (suction device)
M Workpiece mixture m1 Recyclable granules (reusable abrasive)
m2 Industrial waste powder (including lightweight foreign materials and abrasive powdered by wear)
X granular material separation processing device (Example device)

4a Flexible bag container (flexible bag)
4b Flexible bag container (flexible bag)
8 Hopper tank device 81 Bag filter 82 Screw feeder 9 Portable machine frame (platform)
Z Powder separation and recovery system (Example system)

Claims (12)

  1.  比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を系内導入し、乾式で前記粉粒体と前記軽量異物類とを分離処理する粉粒体分離処理装置において、
    集塵装置や電気掃除機等の外部吸引機器に接続した分離処理容器に前記被処理混合物を吸引導入し、該容器内で流動を制御しながら気流と比重差を利用して分離処理し、前記粉粒体を系内回収するとともに、前記軽量異物類を前記外部吸引機器に向けて系外排出するための粉粒体分離処理装置であって、
    前記粉粒体を回収貯留するホッパタンクと、該ホッパタンクの上部構造として被冠封着され周面に前記被処理混合物を受け入れる吸引導入管と、上面に前記外部吸引機器に接続する吸引排出管を設けた分離処理容器を備えるとともに、
    前記分離処理容器が、漏斗状に底面形成した分離コーンと、該分離コーンの先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口を有してなり、
    前記吸引排出管が、その先端部を多重管構成とし、それぞれの軸芯を前記分離コーンの回転軸(円錐軸)に合致させ、かつ、それらの管径を前記筒口の各口径に対応する小径なものとして遊挿して開口端部に臨ませてなり、
    前記分離処理容器内に吸引導入した前記被処理混合物を前記筒口に向けて落下誘導するとともに、前記吸引排出管により軽量異物類を多段階に吸引して系外排出し、残る粉粒体を系内に落下回収するようにしたことを特徴とする粉粒体分離処理装置。
    Introducing into the system a mixture in which a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several mm or less, and light-weight foreign substances accompanying the mixture are mixed, In the granular material separation processing apparatus for separating the granular material and the lightweight foreign substances in a dry manner,
    The mixture to be treated is sucked and introduced into a separation processing container connected to an external suction device such as a dust collector or a vacuum cleaner, and is separated using an air flow and a specific gravity difference while controlling flow in the container, A powder separation processing device for collecting powder particles in the system and discharging the lightweight foreign substances out of the system toward the external suction device,
    A hopper tank that collects and stores the granular material, a suction introduction pipe that is crown-sealed as an upper structure of the hopper tank and receives the mixture to be treated on a peripheral surface, and a suction discharge pipe that is connected to the external suction device on the upper surface A separate processing container,
    The separation processing container has a separation cone formed in a funnel-shaped bottom surface, and a cylindrical mouth that hangs downwardly from the tip of the separation cone and has a multi-stage formed by reducing its diameter stepwise.
    The suction / discharge pipe has a multi-tube configuration at its tip, and each axis is aligned with the rotation axis (conical axis) of the separation cone, and the pipe diameter is a small diameter corresponding to each diameter of the tube opening It is loosely inserted as a thing and it faces the opening end,
    The mixture to be treated sucked and introduced into the separation processing container is guided to drop toward the tube port, and light foreign matters are sucked in multiple stages by the suction and discharge pipe and discharged out of the system, and the remaining powder particles are discharged into the system. A granular material separation processing apparatus characterized by being dropped and collected inside.
  2.  分離コーンが、内表面に複数の弾性体からなる整流リブを放射形成したものである請求項1記載の粉粒体分離処理装置。 2. The granular material separation processing apparatus according to claim 1, wherein the separation cone is formed by radiating rectification ribs made of a plurality of elastic bodies on the inner surface.
  3.  被処理混合物が、乾式エアーブラスト装置によるブラスト工程を経たものである請求項1記載の粉粒体分離処理装置。 The granular material separation treatment apparatus according to claim 1, wherein the mixture to be treated has undergone a blasting process using a dry air blasting apparatus.
  4.  集塵装置や電気掃除機等の外部吸引機器に接続され、乾式エアーブラスト装置によるブラスト工程を経た研削材からなる粉粒体と、これに同伴される軽量異物類からなる被処理混合物を分離処理容器内に吸引導入し、該容器内で流動を制御しながら乾式で気流と比重差を利用して分離処理し、前記粉粒体を系内回収するとともに、前記軽量異物類を前記外部吸引機器に向けて系外排出する粉粒体分離処理装置であって、
    前記分離処理容器が、前記粉粒体を回収貯留するホッパタンクと、該ホッパタンクの上部構造として被冠封着され周面に前記被処理混合物を受け入れる吸引導入管と、上面に前記外部吸引機器に接続する吸引排出管を備えるとともに、
    該分離処理容器の底面を漏斗状に形成した分離コーンと、該分離コーンの先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口を有してなり、
    前記吸引排出管が、その先端部を多重管構成とし、それぞれの軸芯を前記分離コーンの回転軸(円錐軸)に合致させ、かつ、それらの管径を前記筒口の各口径に対応する小径なものとして遊挿して開口端部に臨ませてなり、
    前記分離処理容器内に吸引導入した前記被処理混合物を前記筒口に向けて落下誘導するとともに、前記吸引排出管により軽量異物類を多段階に吸引して系外排出し、残る粉粒体を自由落下させて系内回収するようにしたことを特徴とする粉粒体分離処理装置。
    Separation treatment of powdered particles made of abrasives that are connected to external suction devices such as dust collectors and vacuum cleaners, and subjected to a blasting process using a dry air blasting device, and to-be-processed mixtures made up of light foreign substances Introducing suction into a container, separating while utilizing the air flow and the specific gravity difference while controlling the flow in the container, collecting the granular material in the system, and removing the light foreign matter from the external suction device It is a granular material separation processing device for discharging out of the system toward the
    The separation processing container is connected to a hopper tank for collecting and storing the powder and particles, a suction inlet pipe sealed as a top structure of the hopper tank and receiving the mixture to be processed on the peripheral surface, and the external suction device on the upper surface A suction discharge pipe that
    A separation cone having a bottom surface of the separation processing vessel formed in a funnel shape, and a cylindrical mouth that hangs downwardly from the tip of the separation cone and has a multi-step formed by reducing its diameter stepwise,
    The suction / discharge pipe has a multi-tube configuration at its tip, and each axis is aligned with the rotation axis (conical axis) of the separation cone, and the pipe diameter is a small diameter corresponding to each diameter of the tube opening It is loosely inserted as a thing and it faces the opening end,
    The mixture to be treated that has been sucked into the separation container is guided to drop toward the tube port, and lightweight foreign substances are sucked in multiple stages through the suction discharge pipe and discharged outside the system, and the remaining powder particles are free. A granular material separation processing apparatus, wherein the apparatus is dropped and collected in the system.
  5.  分離コーンが、内表面に複数の弾性体からなる整流リブを放射形成したものである請求項4記載の粉粒体分離処理装置。 5. The granular material separation processing apparatus according to claim 4, wherein the separation cone is formed by radiating rectifying ribs made of a plurality of elastic bodies on the inner surface.
  6.  請求項1乃至5のいずれか1項記載の粉粒体分離処理装置において、
    分離処理容器内で分離コーンによる被処理混合物の落下誘導と吸引排出管による軽量異物類の吸引排出とを協働させて流動を制御しながら粉粒体と軽量異物類とを分離処理するよ
    うにした粉粒体分離処理方法であって、
    吸引導入により受け入れた前記被処理混合物を前記分離処理容器内で発生する気流を利用して軽重分離しながら、前記分離コーンの内表面に受け止めて旋回と落下を一旦阻止し、跳ね返りを含む爾後の自由落下に任せ、前記分離コーンの筒口に向けてカスケード状に落下誘導しながら、前記吸引排出管により軽量異物類を多段階に吸引して系外排出し、残る粉粒体を落下回収するようにしたことを特徴とする粉粒体分離処理方法。
    In the granular material separation processing apparatus according to any one of claims 1 to 5,
    In the separation container, the powder and light foreign substances are separated from each other while controlling the flow by collaborating the drop induction of the mixture to be treated by the separation cone and the suction and discharge of the light foreign substances by the suction / discharge pipe. A method for separating powder particles,
    While lightly separating the mixture to be treated received by introduction of suction using an air flow generated in the separation processing container, it is received on the inner surface of the separation cone to temporarily stop swirling and falling, and includes rebounding While letting it fall freely, inducing a drop in a cascade toward the cylinder mouth of the separation cone, lightweight foreign substances are sucked out in multiple stages by the suction / discharge pipe and discharged out of the system, and the remaining granular material is dropped and collected A method for separating a granular material, characterized by comprising:
  7.  被処理混合物の落下誘導を増補するために、分離コーンの内表面に複数の弾性体からなる整流リブを放射形成して被処理混合物を受け止めるようにした請求項6記載の粉粒体分離処理方法。 7. A method for separating a granular material according to claim 6, wherein in order to augment the drop induction of the mixture to be treated, a flow straightening rib made of a plurality of elastic bodies is formed on the inner surface of the separation cone to receive the mixture to be treated. .
  8.  集塵装置や電気掃除機等の外部吸引機器に接続され、乾式エアーブラスト装置によるブラスト工程を経た研削材からなる粉粒体と、これに同伴される軽量異物類からなる被処理混合物を分離処理容器内に吸引導入し、該容器内で流動を制御しながら気流と比重差を利用して乾式で分離処理し、前記粉粒体を系内回収するとともに、前記軽量異物類を前記外部吸引機器に向けて系外排出するために、前記分離処理容器が、前記粉粒体を回収貯留するホッパタンクと、該ホッパタンクの上部構造として被冠封着され周面に前記被処理混合物を受け入れる吸引導入管と、上面に前記外部吸引機器に接続する吸引排出管を備えてなる粉粒体分離処理装置において、
    前記分離処理容器の底面を漏斗状に形成した分離コーンと、該分離コーンの先端部から下向き凸状に垂下し、その口径を階段的に減少させた筒口を多段形成するとともに、
    前記吸引排出管の先端部を多重管構成とし、それぞれの軸芯を前記分離コーンの回転軸(円錐軸)に合致させ、かつ、それらの管径を前記筒口の各口径に対応する小径なものとして遊挿して開口端部に臨ませてなり、
    前記分離処理容器内で前記分離コーンによる前記被処理混合物の落下誘導と前記吸引排出管による前記軽量異物類の吸引排出とを協働させて流動を制御しながら前記粉粒体と前記軽量異物類とを分離処理するようにした粉粒体分離処理方法であって、
    吸引導入により受け入れた前記被処理混合物を前記分離処理容器内で発生する気流を利用して軽重分離しながら、前記分離コーンの内表面に受け止めて旋回と落下を一旦阻止し、跳ね返りを含む爾後の自由落下に任せ、前記筒口に向けてカスケード状に落下誘導しながら、前記吸引排出管により軽量異物類を多段階に吸引して系外排出し、残る粉粒体を落下回収するようにしたことを特徴とする粉粒体分離処理方法。
    Separation treatment of powdered particles made of abrasives that are connected to external suction devices such as dust collectors and vacuum cleaners, and subjected to a blasting process using a dry air blasting device, and to-be-processed mixtures made up of light foreign substances Introducing suction into the container, using the air flow and the difference in specific gravity to separate the powder while controlling the flow in the container, and recovering the powder particles in the system, and removing the light foreign matter from the external suction device A hopper tank that collects and stores the granular material, and a suction introduction pipe that is crown-sealed as an upper structure of the hopper tank and receives the mixture to be treated on its peripheral surface. And in the granular material separation processing apparatus comprising a suction discharge pipe connected to the external suction device on the upper surface,
    A separation cone in which the bottom surface of the separation processing vessel is formed in a funnel shape, and a downwardly projecting downward from the tip of the separation cone, and a multi-stage tube opening with a reduced diameter is formed in stages.
    The suction and discharge pipe has a multi-tube configuration at the tip, each axis is aligned with the rotation axis (conical axis) of the separation cone, and the pipe diameter is small corresponding to each diameter of the tube opening As a loose insertion and facing the opening end,
    In the separation processing container, the powder particles and the lightweight foreign matters are controlled while controlling the flow by cooperating the fall induction of the mixture to be treated by the separation cone and the suction and discharging of the lightweight foreign matters by the suction and discharge pipe. And a granular material separation treatment method, wherein
    While lightly separating the mixture to be treated received by introduction of suction using an air flow generated in the separation processing container, it is received on the inner surface of the separation cone to temporarily stop swirling and falling, and includes rebounding It was left to free fall, and while guiding the fall in a cascade toward the tube opening, lightweight foreign substances were sucked out in multiple stages by the suction discharge pipe and discharged out of the system, and the remaining granular material was dropped and collected A granular material separation treatment method.
  9.  被処理混合物の落下誘導を増補するために、分離コーンの内表面に複数の弾性体からなる整流リブを放射形成して被処理混合物を受け止めるようにした請求項8記載の粉粒体分離処理方法。
    9. The method for separating a granular material according to claim 8, wherein in order to augment the drop induction of the mixture to be treated, a flow straightening rib made of a plurality of elastic bodies is formed on the inner surface of the separation cone to receive the mixture to be treated. .
  10.  比重や硬度が比較的大きく粒径が数mm以下のグリット状又はショット状の初期形状からなる粉粒体と、これに同伴される軽量異物類が混ざり合った被処理混合物を吸引導入し、乾式で前記粉粒体と前記軽量異物類とを分離処理する粉粒体分離処理装置を包含し、該粉粒体分離処理装置にバキューム接続する前・後流の連係機器又は連係装置をプラットフォームとなる単一の枠体内に収設し、かつ、工程順にライン配置して系統的な処理をおこなうようにした粉粒体分離回収処理システムであって、
    系外より被処理混合物を受け入れて一時貯留するための第1の工程処理を担当するホッパタンク装置と、
    前記ホッパタンク装置から移送導入され、乾式で前記被処理混合物を構成する比較的粒径の大きいリサイクル可能粒体と比較的粒径の小さい産廃粉体及び軽量異物類とに分離処理するための第2の工程処理を担当する粉粒体分離処理装置と、
    前記粉粒体分離処理装置の下段に脱着交換可能に設置され、分離処理後のリサイクル可能
    粒体を落下回収して貯留するための柔軟性袋体容器と、
    前記粉粒体分離処理装置から配管導入され、分離処理後の廃棄粉体及び軽量異物類と粉塵とを分別処理するための第3の工程処理を担当する集塵サイクロン装置と、
    前記集塵サイクロン装置の下段に脱着交換可能に設置され、分別処理後の前記産廃粉体及び軽量異物類を落下回収して貯留するための柔軟性袋体容器と、
    前記集塵サイクロン装置と配管接続され、装置系のバキューム経路の駆動源となるとともに、分別処理後の粉塵を吸引導入して最終的に捕捉するための第4の工程処理を担当する電気掃除機その他の吸引装置と、
    前記柔軟性袋体容器を含む装置群を工程順にライン配置して、単一のフレーム又はケーシング内に収設し、1ライン又は並列する複数ラインの処理系統からなる装置系ユニットを構設するとともに、輸送可能で現場設置可能なプラットフォームとして用いるための可搬性機枠を具備してなり、
    前記装置系ユニットを稼働させて前記第1乃至第4の工程処理を系統的に、かつ、系内で処理するようにしたことを特徴とする粉粒体分離回収処理システム。
    Suction and introduction of a mixture to be treated, in which a granular material having a grit-like or shot-like initial shape having a relatively large specific gravity and hardness and a particle size of several millimeters or less, and light-weight foreign substances accompanying it, is introduced and dried. Including a granular material separation processing device that separates the granular material and the light-weight foreign matter, and a platform is used as a front-rear linking device or a linking device that is vacuum connected to the granular material separation processing device. It is a granular material separation and recovery processing system that is placed in a single frame and arranged in a line in the order of processes to perform systematic processing,
    A hopper tank device in charge of the first process for receiving and temporarily storing the mixture to be treated from outside the system;
    A second process for separating and processing into recyclable granules having a relatively large particle size, industrial waste powder and light-weight foreign matters having a relatively small particle size, which are transferred from the hopper tank apparatus and constitute the mixture to be treated in a dry manner. A granular material separation processing device in charge of the process of
    A flexible bag container that is installed in the lower stage of the powder and particle separation apparatus so that it can be removed and replaced, and drops and collects the recyclable particles after the separation process,
    A dust collecting cyclone apparatus in charge of a third process for separating and processing waste powder and light-weight foreign substances and dust after being piped from the granular material separation processing apparatus;
    A flexible bag container that is installed in the lower stage of the dust collection cyclone device so as to be removable and replaceable, and that collects and collects the industrial waste powder and the lightweight foreign matters after the separation process, and
    A vacuum cleaner connected to the dust collecting cyclone device and serving as a drive source for the vacuum path of the device system, and in charge of the fourth process for sucking and finally capturing the dust after the separation process With other suction devices,
    The apparatus group including the flexible bag container is arranged in a line in the order of processes, and is arranged in a single frame or casing, and an apparatus system unit including one line or a plurality of lines of parallel processing systems is constructed. A portable machine frame for use as a platform that can be transported and installed on-site,
    A granular material separation and recovery processing system, wherein the apparatus system unit is operated to perform the first to fourth process processes systematically and within the system.
  11.   粉粒体分離処理装置が、粉粒体を回収貯留するホッパタンク部と、該ホッパタンク部の上部構造として被冠封着され周面に被処理混合物を受け入れる吸引導入管と、上面に吸引機器に接続する吸引排出管を設けた分離処理容器を備えるとともに、該分離処理容器が、漏斗状に底面形成した分離コーンと、該分離コーンの先端部から下向き凸状に垂下し、その口径を階段的に減少させて多段形成した筒口を有してなり、
    前記吸引排出管が、その先端部を多重管構成とし、それぞれの軸芯を前記分離コーンの回転軸(円錐軸)に合致させ、かつ、それらの管径を前記筒口の各口径に対応する小径なものとして遊挿して開口端部に臨ませてなり、
    前記分離処理容器内に吸引導入した前記被処理混合物を前記筒口に向けて落下誘導するとともに、前記吸引排出管により軽量異物類を多段階に吸引して後流の集塵サイクロン装置へ排出し、残る粉粒体を柔軟性袋体容器に落下回収するようにしたものである請求項11記載の粉粒体分離回収処理システム。
    The powder separation processing device is connected to a hopper tank part for collecting and storing the powder, a suction inlet pipe sealed as a top structure of the hopper tank part and receiving the mixture to be treated on the peripheral surface, and a suction device on the upper surface A separation processing container provided with a suction / discharge pipe, and the separation processing container is formed in a funnel-like shape with a bottom formed in a bottom surface, and is projected downward from the tip of the separation cone in a stepwise manner. It has a tube port formed in multiple stages by reducing,
    The suction / discharge pipe has a multi-tube configuration at its tip, and each axis is aligned with the rotation axis (conical axis) of the separation cone, and the pipe diameter is a small diameter corresponding to each diameter of the tube opening It is loosely inserted as a thing and it faces the opening end,
    Inducing and dropping the mixture to be treated sucked into the separation processing container toward the tube port, the suction discharge pipe sucks lightweight foreign substances in multiple stages and discharges them to the downstream dust collecting cyclone device, 12. The granular material separation and recovery processing system according to claim 11, wherein the remaining granular material is dropped and collected in a flexible bag container.
  12.  被処理混合物が、乾式エアーブラスト装置によるブラスト工程を経たものであり、直接又は一時貯留してホッパタンク装置に圧送供給されるものである請求項10又は11記載の粉粒体分離回収処理システム。 12. The granular material separation and recovery processing system according to claim 10 or 11, wherein the mixture to be treated has been subjected to a blasting process by a dry air blasting device, and is directly or temporarily stored and pumped and supplied to the hopper tank device.
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